Electrode catalyst for electrolytic reduction of carbon dioxide gas

ABSTRACT

An electrocatalyst for use in electrolytic reduction of carbon dioxide gas in an aqueous solution. The electrocatalyst is formed of nickel alkyl cyclam which is expressed by the general formula: ##STR1## where each of R 1 , R 2 , R 3 , R 4 , R 5  and R 6  is selected from the group consisting of hydrogen atom and aliphatic saturated hydrocarbon group expressed by the formula of C n  H 2n+1  ; wherein at least one of R 1 , R 2 , R 3 , R 4 , R 5  and R 6  is the aliphatic saturated hydrocarbon group in which n is a number ranging from 1 to 22. The nickel alkyl cyclam as the electrocatalyst is excellent in stability and energy consumption improving effect while exhibiting a high carbon dioxide gas reduction effect, as compared with conventional nickel cyclam.

BACKGROUND OF THE INVENTION

1. Field of the Invention

This invention relates to improvements in an electrocatalyst for electrolytic reduction of carbon dioxide gas (CO₂).

2. Description of the Prior Art

Attention is being paid to researches and developments relating to reduction fixation and recovery of carbon dioxide gas, which are disclosed for example in Japanese Patent Provisional Publication No. 64-15388. These researches and developments include ones relating to electrochemical reduction of carbon dioxide gas in which a reduction by using an electrolysis catalyst is used for the purpose of improving selectivity in reaction. The reduction catalyst is used in the state to modify the surface of an electrode of metal, or to be added in an electrolyte solution. It is known that examples of such a reduction catalyst are metallophanine complexes and nickel macrocyclic polyamine complexes.

Additionally, it is disclosed that nickel cyclam (1,4,8,11-tetraazatetradecane) serves as an electrocatalyst for reducing carbon dioxide to carbon monoxide with a high reaction selectivity even in an aqueous solution in "Journal of the American Chemical Society", 1986, 108, 7461-7467.

However, the following difficulties have been encountered in the conventional electrocatalyst of nickel cyclam: (a) An effect of decreasing the overvoltage is low, thereby increasing energy consumption. (b) The turnover number for the catalyst is low. (3) The stability of the catalyst is low. (4) In the aqueous electrolyte solution, a hydrogen gas generation reaction and a carbon dioxide reduction reaction compete with each other, so the selectivity of reactions is insufficient. Thus, the conventional electrode catalyst of nickel cyclam is insufficient for practical use in electrolytic reduction of carbon dioxide gas in an aqueous solution.

SUMMARY OF THE INVENTION

An object of the present invention is to provide an improved electrocatalyst for electrolytic reduction of carbon dioxide gas in aqueous solution, by which difficulties encountered in conventional similar electrocatalysts can be effectively overcome.

Another object of the present invention is to provide an improved electrocatalyst for electrolytic reduction of carbon dioxide gas in an aqueous solution, which is high in reaction selectivity and stability while the turnover number therefor being high.

Hitherto, it is known that in the case where alkyl group(s) is introduced into a nickel cyclam, the reactivity of the nickel cyclam with other groups is decreased because of steric hindrance of the introduced alkyl group(s) regardless of C-substitution or N-substitution for the introduced alkyl group(s). By analogy on the basis of the above, it will be expected that it is better not to carry out the substitution with the alkyl group(s). However, it is to be noted that it has been confirmed that some nickel alkyl cylams exhibit a carbon dioxide gas reduction ability equal to or higher than nickel cyclam. Thus, upon selecting the number of alkyl groups, introduction of alkyl groups acts advantageously from the catalytic view point over the above disadvantage of the steric hindrance. Furthermore, attention should be paid to the fact that the difficulties in the conventional nickel cyclam as the electrocatalyst can be solved by introducing alkyl group(s) into the nickel cyclam. The above was confirmed by the present inventors, which has led the inventors to realization of the present invention.

Thus, the electrocatalyst of the present invention is for electrolytic reduction of carbon dioxide gas in an aqueous solution and is expressed by the general formula: ##STR2## where each of R₁, R₂, R₃, R₄, R₅ and R₆ is selected from the group consisting of hydrogen atom and aliphatic saturated hydrocarbon group expressed by the formula of C_(n) H_(2n+1) ; and at least one of R₁, R₂, R₃, R₄, R₅ and R₆ is the aliphatic saturated hydrocarbon group in which n is a number ranging from 1 to 22.

Introduction of alkyl group(s) in the structure of the cyclam provides the electrocatalyst for CO₂ reduction is high in stability and reaction selectivity and less in energy consumption in electrolysis, while exhibiting a high reduction effect to carbon dioxide gas. Thus, this electrocatalyst industrially highly valuable.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a graph showing a cyclic voltammograms of a nickel alkyl cyclam of Example under N₂ and CO₂ according to the present invention;

FIG. 2 is a graph similar to FIG. 1 but showing cyclic voltammograms of another nickel alkyl cyclam of Example 2 according to the present invention;

FIG. 3 is a graph similar to FIG. 1 but showing a cyclic voltammogram of a further nickel alkyl cyclam of Example 3 according to the present invention;

FIG. 4 is a graph showing a cyclic voltammogram of conventional nickel cyclam; and

FIG. 5 is an enlarged sectional view showing a state in which the nickel alkyl cyclam of the present invention is adsorbed on the surface of an electrode in an electrolyte solution during an electrolytic reduciton of carbon dioxide gas.

DETAILED DESCRIPTION OF THE INVENTION

According to the present invention, an electrocatalyst for electrolyte reduction of carbon dioxide gas is expressed by the general formula: ##STR3## where each of R₁, R₂, R₃, R₄, R₅ and R₆ is selected from the group consisting of hydrogen atom and aliphatic saturated hydrocarbon group expressed by the formula of C_(n) H_(2n+1) ; and at least one of R₁, R₂, R₃, R₄, R₅ and R₆ is the aliphatic saturated hydrocarbon group in which n is a number ranging from 1 to 22.

The electrocatalyst of the present invention is formed of nickel alkyl cyclam which is a derivative of nickel cyclam. Such nickel alkyl cyclam can be produced by a method as disclosed in a technical literature "Tetrahedron Lett.", 12, 1049 (1977), in which each of R₁ and R₂ in the formala (1) is aliphatic hydrocarbon group. In this production method, the nickel alkyl cyclam is obtained by reducing 3-alkyl-2,4-dioxo-1,5,8,12-tetraazacyclotetradecane with diborane. The 3-alkyl-2,4-dioxotetraazacyclotetradecane is obtained by a condensation reaction between alkylmalonic diester and 1,4,8,11-tetraazaundecane. Additionally, a nickel alkyl cyclam having aliphatic hydrocarbon at the positions of R₃, R₄, R₅ and R₆ in the formula (1) can be produced by a method disclosed in technical literatures "Inorg. Chem.", 1986, 25, 4131-4135 and 1987, 26, 3527-3533. Otherwise, the nickel alkyl cyclam can be produced by alkylation of nickel cyclam with alkyl halide.

In technical literature "J. Am. Chem. Soc.", 1986, 108, 7461-7467, it is suggested that the nickel cyclam adsorbed on the surface of an electrode plays an important role in electolytic reduction of carbon dioxide. This technical literature discloses a measurement of oxidation-reduction wave of Ni(II)/Ni(I) redox coupled cyclic voltammetry using a mercury electrode under saturated nitrogen, in which an oxidation-reduction wave (diffusion controlled wave) due to diffusion of the nickel cyclam from a solution is mainly observed. While another oxidation-reduction wave (adsorption wave) due to adsorption of Ni(II)ad/Ni(I)ad redox couple the surface of the electrode appears as a prewave which has been slightly shifted toward anodic potential or to a more positive potential relative to the above-mentioned diffusion controlled wave. The diffusion control wave appears at E_(1/2) (half-wave potential)=1,56 V versus a saturated calomel electrode, while the adsorption wave appears at E_(1/2) =1.35 V. In the above, Ni(II)/Ni(I) represents a redox couple of Ni having a valence of +2 and Ni having a valence of +1 in the nickel cyclam. Additionally, the Ni(II)ad/Ni(I)ad represents the above-mentioned redox couple of the nickel cyclam adsorbed on the surface of the electrode.

Under the fact that an adsorbed species on the surface of the electrode plays an important role in electrolytic reduction of carbon dioxide gas, it is preferable that )a) the adsorbtion wave is clearly separate from the diffusion controlled wave, and (b) both the waves are shifted toward anodic potentials.

It is to be noted that the nickel alkyl cyclam as the electrocatalyst of the present invention meets the above conditions (a) and (b). In other words, the adsorption wave of the nickel alkyl cyclam of the present invention is observed more clearly than that of the conventional nickel cyclam in a cyclic voltammogram obtained by a cyclic voltammetry. This demonstrates that the nickel alkyl cyclam is stably adsorbed onto the surface of the electrode, which is effective for the electrolytic reduction of carbon dioxide gas.

It has been apparent that in the nickel alkyl cyclam having (substituted) alkyl groups respectively at the positions of R₃, R₄, R₅ and R₆, the potentials of both the adsorption wave and diffusion controlled wave are largly shifted toward anodic potential number of the substituent groups increases. This deminutes over voltages for the reduction reaction of carbon dioxide gas, thereby reducing energy consumption. Additionally, such decrease in applied voltage in an aqueous solution suppresses generation of hydrogen gas competing with carbon dioxide gas reduction, thus providing a high selectivity of the carbon dioxide reduction. Accordingly, within a range reaching the thermodynamically determined reduction potential of carbon dioxide, the anodic shifts of the potential of the adsorption wave and the diffusion controlled wave are effective for lowering energy consumption and for high selectivity of carbon dioxide reduction reaction. As will be appreciated from the above, the nickel alkyl cyclam of the present invention is more excellent as an electrode catalyst for electrolytic reduction of carbon dioxide, than the conventional nickel cyclam.

In the nickel alkyl cyclam of the present invention, the solubility thereof to water changes according to the magnitude of n in the aliphatic saturated hydrocarbon (C_(n) H_(2n+1)). More specifically, it is judged that when n is within a range from 1 to about 6, the nickel alkyl cyclam is soluble in water; When n is not less than 14, it is insoluble in water; and When n is between about 6 and 14, it becomes a surface active agent. Of these nickel alkyl cyclams, one soluble in water is used as the electrocatalyst upon being formed into an aqueous electrolyte solution. Otherwise, one insoluble in water can be also used as the electrocatalyst upon being adsorbed onto the surface of the electrode by a Langmuir-Blodgett technique. The electrode on which the electrocatalyst is adsorbed is preferably formed of a material high in hydrogen overvoltage, such as mercury, gold amalgam, lead, tin or cadmium.

In order to evaluate the electrocatalyst for electolytic reduction of carbon dioxde gas, according to the present invention, Examples and Experiment will be discussed hereafter.

EXAMPLE 1

Cyclic voltammetry was conducted for a sodium hydrogen carbonate buffer solution (ph=6.2) containing 1 mM of nickel alkyl cyclam (R₁ =C₂ H₅ ; and R₂, R₃, R₄, R₅ and R₆ =H), 0.1M of sodium perchlorate (NaClO₄) as an electrolyte, under N₂ thereby to obtain a cyclic voltammogram (A) in FIG. 1, and under CO₂ saturation thereby to obtain another cyclic voltammogram (B) in FIG. 1. In the above cyclic voltammetries measurements, a gold amalgam electrode was used as a working electrode; a saturated calomel electrode (SCE) as a reference electrode; and a glassy carbon electrode as a counter electrode.

As shown in the cyclic voltammogram (A) in FIG. 1, the adsorption wave due to oxidation-reduction of Ni(II)ad/Ni(I)ad of the nickel alkyl cyclam was clearly appeared at 1.36 V, which demonstrated that the nickel alkyl cyclam was firmly adsorbed on the surface of the electrode. Additionally, as shown in the cyclic voltammogram (B) in FIG. 1, the reduction current sharply increased from -1.14 V, which demonstrated that the nickel alkyl cyclam of this Example exhibited an excellent reduction ability to carbon dioxide gas.

EXAMPLE 2

Cyclic voltammetry was conducted in the way as those in Example 1 with the exception that used nickel alkyl cyclam (1 mM concentration) was of the type wherein R₁ =CH₃ ; and R₂, R₃, R₄, R₅ and R₆ =H, under N₂ saturation thereby to obtain a cyclic voltammogram (A) in FIG. 2, and under CO₂ saturation thereby to obtain another cyclic voltammogram (B) in FIG. 2.

As shown in the cyclic voltammogram (A) in FIG. 2, the adsorption wave due to oxidation-reduction of Ni(II)ad/Ni(I)ad of the nickel alkyl cyclam clearly appeared at 1.36 V, which demonstrated that the nickel alkyl cyclam was firmly adsorbed on the surface of the electrode. Additionally, as shown in the cyclic voltammogram (B) in FIG. 2, the reduction current sharply increased from -1.08 V, which demonstrated that the nickel alkyl cyclam of this Example exhibited an excellent reduction ability to carbon dioxide gas.

EXAMPLE 3

Cyclic voltammetry was conducted in the way as those in Example 1 with the exception that used nickel alkyl cyclam was of the type wherein R₃ =CH₃ ; and R₁, R₂, R₄, R₅ and R₆ =H, and the concentration of the nickel alkyl cyclam was 0.1 mM, under N₂ saturation thereby to obtain a cyclic voltammogram (A) in FIG. 3 and under CO₂ saturation thereby to obtain another cyclic voltammogram (B) in FIG. 3.

As shown in the cyclic voltammogram (A) in FIG. 3, the adsorption wave due to oxidation-reduction of Ni(II)ad/Ni(I)ad of the nickel alkyl cyclam clearly appeared, which demonstrated that the nickel alkyl cyclam was firmly adsorbed on the surface of the electrode. Additionally, the diffusion controlled wave and the adsorption wave were anode-shifted respectively 100 mV and 90 mV as appreciated upon comparison with a cyclic voltammogram of the conventional nickel cyclam in FIG. 5. Furthermore, as shown in the cyclic voltammogram (B) in FIG. 3, the electrolytic reduction of carbon dioxide was stably carried out at the peak potential (E=1.22 V) of the adsorption wave.

EXPERIMENT

A controlled potential electrolysis (E=-1.29 V) of an electrolyte solution containing each nickel alkyl cyclam (used in Examles 1, 2 and 3) or nickel cyclam was carried out for three hours to make an electrolytic reduction of carbon dioxide, under the following conditions:

Concentration of nickel alkyl cyclam or nickel cyclam: 1 mM;

Electrolyte solution: a solution containing NaClO₄ (0.1M) and NaHCO₃ (35 mM) having a pH of 6.2;

Electrode: a gold amalgam electrode (electrode surface=0.018 cm²); and

Atmosphere: CO₂.

In the above experiment, so-called turnover number was determined for each of the nickel alkyl cyclam and the nickel cyclam when carbon dioxide was electrolytically reduced. The turnover number was a value obtained by dividing the quantity of electricity passed through the electrode by the concentration of the nickel alkyl cyclam or the nickel cyclam. The turnover numbers of the respective cyclams were compared with each other as relative values as shown in Table 1. The experimental results of Table 1 demonstrate that the nickel alkyl cyclams of the present invention serve as excellent electrode catalysts for electrolytic reduction of carbon dioxide gas.

                  TABLE 1                                                          ______________________________________                                                              Turnover number                                           Sample               (relative value)                                          ______________________________________                                         Nickel cyclam        1                                                         Nickel alkyl cyclam in Example 1                                                                    2.2                                                       Nickel alkyl cyclam in Example 2                                                                    2.0                                                       Nickel alkyl cyclam in Example 3                                                                    1.3                                                       ______________________________________                                    

In this experiment, the nickel alkyl cyclam 1 was adsorbed on the surface of the electrode 2 and in contact with the electrolyte solution 3 as shown in FIG. 5 in which the electrode 2 with the nickel alkyl cyclam 1 is illustrated in an enlarged cross-section.

As discussed above, the redox potential of Ni(II)/Ni(I) of the nickel alkyl cyclam is shifted toward anode potential as compared with that of the conventional nickel cyclam. Such an anodic shift phenomena lowers the applied voltage during the electrolytic reduction of CO₂ thereby reducing the overvoltage. The reduction of overvoltage is the most important in performance of electrocatalyst.

The anodic shift phenomena can increase stability of nickel cyclam. The reason for this is as follows: As the applied voltage increases, the electrolysis current increases whereas nickel tends to be easily get out of the cyclam. It is to be noted that the nickel separated from the cyclam does not have an ability of reducing CO₂. Accordingly, the nickel alkyl cyclam can be used as a stable electrocatalyst when the redox potential is shifted anodically.

Additionally, as discussed above, the nickel alkyl cyclam adsorbed on the surface of the electrode plays an important role in the electrolytic reduction of CO₂. This adsorbed nickel alkyl cyclam is observed as the adsorption wave in a current-voltage curve. It is to be noted that this adsorption wave is observed very clearly as compared with that of the conventional nickel cyclam, particularly as shown in the voltammogram (A) in FIG. 3 in which the adsorption wave of the nickel alkyl cyclam was observed as a wave having a sharp peak. This demonstrated a strong and stable adsorption of the nickel alkyl cyclam onto the surface of the electrode, which seems to provide an excellent CO₂ reduction ability. In contrast, the corresponding adsorption wave of the nickel cyclam could not be observed so clealy as shown in FIG. 4. Thus, the adsorption condition of nickel cyclam onto the electrode is further improved by introducing alkyl group(s) thereinto.

Such introduction of alkyl group(s) can make nickel cyclam an amphipathic compound. As a result, the nickel alkyl cyclam is not only used as the electrocatalyst upon being added into a solution, but also used as a variety of molecular aggregates such as a monomolecular film, a bimolecular film, a micell, a vesicle and a liquid crystal. Additionally, the nickel alkyl cyclam may be used as a variety of functional organic materials. Hence, it will be appreciated that the nickel alkyl cyclam is highly effective and excellent in electrolytic reduction of carbon dioxide over the conventional nickel cyclam. 

What is claimed is:
 1. An electrocatalyst for electrolytic reduction of carbon dioxide gas in an aqueous solution, said electrocatalyst being expressed by the general formula: ##STR4## where each of R₁, R₂, R₃, R₄, R₅, and R₆ is selected from the group consisting of a hydrogen atom and an aliphatic saturated hydrocarbon group expressed by the formula of C_(n) H_(2n+1) ; in which n is a number ranging from 1 to 22, with the proviso that at least one of R₁ -R₆ is an aliphatic saturated hydrocarbon group having an n value of greater than or equal to about
 6. 2. An electrocatalyst as claimed in claim 1, where only one of R₁, R₂, R₃, R₄, R₅ and R₆ is the aliphatic saturated hydrocarbon group, the others being respectively hydrogens.
 3. An electrocatalyst as claimed in claim 1, wherein said electrocatalyst is in contact with a surface of an electrode used for an electrolytic reduction of carbon dioxide.
 4. An electrode catalyst as claimed in claim 3, wherein said electrode is made of a material selected from the group consisting of mercury, gold, amalgam, lead, tin and cadmium.
 5. An electrocatalyst as claimed in claim 3, wherein each of R₃, R₄, R₅, and R₆ are aliphatic saturated hydrocarbon groups.
 6. A composition comprising the catalyst of claim 1 and an aqueous solution.
 7. A composition as claimed in claim 6, wherein in at least one of the R groups n is from 6 to
 14. 8. A composition as claimed in claim 6, further comprising an electrolyte.
 9. A composition comprising an electrode having absorbed onto it an electrocatalyst as claimed in claim
 1. 10. A composition as claimed in claim 9, wherein n is greater than about
 14. 11. A composition comprising an electrolyte and an electrocatalyst as claimed in claim
 1. 12. An electrocatalyst as claimed in claim 1, wherein at least two of R₁ -R₆ area aliphatic saturated hydrocarbons.
 13. A composition comprising an electrocatalyst as claimed in claim 1 absorbed onto the surface of an electrode, wherein the electrode is in contact with an electrolyte solution.
 14. An electrocatalyst as claimed in claim 1, wherein at least one of the R groups has an n value of between 6 and
 14. 15. An electrocatalyst as claimed in claim 1, wherein at least one of the R groups has an n value of greater than about
 14. 16. An electrode arrangement used in electrolytic reduction of carbon dioxide in aqueous solution, said electrode arrangement comprising:an electrode in the aqueous solution; and an electrocatalyst formed on a surface of said electrode, said catalyst being expressed by the following general formula: ##STR5## where each of R₁, R₂, R₃, R₄, R₅, and R₆ is selected from the group consisting of a hydrogen atom and an aliphatic saturated hydrocarbon group expressed by the formula of C_(n) H_(2n+1) ; in which n is a number ranging from 1 to 22, with the proviso that at least one of R₁ -R₆ is an aliphatic saturated hydrocarbon group having an n value of greater than or equal to about
 6. 17. An electrode arrangement as claimed in claim 16, wherein said electrode is made of a material selected from the group consisting of mercury, gold amalgam, lead, tin and cadmium.
 18. An apparatus for electrolytic reduction of carbon dioxide comprising:container means in which an aqueous electrolyte solution is contained; an electrode dipped in said aqueous electrolyte solution; an electrocatalyst in contact with a surface of said electrode, said electrocatalyst being expressed by the following formula: ##STR6## where each of R₁, R₂, R₃, R₄, R₅, and R₆ is selected from the group consisting of a hydrogen atom and an aliphatic saturated hydrocarbon group expressed by the formula of C_(n) H_(2n+1) ; in which n is a number ranging from 1 to 22, with the proviso that at least one of R₁ -R₆ is an aliphatic saturated hydrocarbon group having an n value of greater than or equal to about
 6. 19. An apparatus as claimed in claim 18, wherein said aqueous electrolyte solution contains sodium perchlorate and sodium hydrogencarbonate. 